Vaporizer



9ct n i927 F. A. MILLIFF `ET AL vAroRIzER Filed Jan. 11 1926 5 Sheets-Sheet 1 wv MM mk i Y .M d

1,644,937 Oct' 11 1927 F. A. MILLIFF ET Al- VAPORIZER Filed Jan.11v, 192s s sheets-sheet s Patented Oct. 11, 1927.

UNITED- STATES 1,644,937 PATENT OFFICE.

FRANK A. IMILIJIFFVy AND JOHN A MILLIFF, 0]? LOSv NGELES, `CALIFORNIA..

varomznn.

Appncatidn mealanaary 11, 192e. 'serial No- 86,581.

'Our invention relates to petroleum regining apparatus and more particularly t-aran apparatus in which 'the oil is first heated 1n a pipe still or the like and then passed to a Q vaporizerV in which the vapors are separated therefrom. Y Y

In the usual form of such apparatus, the

petroleum is heated in the pipe still to a temperature above the boiling point of the least 10 volatile of the hydrocarbons which it is desired to remove in the first distillation. The

mixture of oil and vapors so produced is then passed into a vaporizer in which the vapors of certain of the hydrocarbons are separated from the residuum, being then passed to suitable condensing elements in which they may be fractionally condensed to produce various commercial products.

In the past one of the chief difficulties experienced by refiners inthe operation of such vaporizers was that they were not susceptible of close control in order to limit the end boiling points of t-he vapor mixture separated therein. Moreover, an undesirable dephlegmating action took place in the lower stage of the vaporizer which'caused some of the more volatile hydrocarbons to be rabsorbed and to pass out with the residuum with consequent loss in values. A further diiiiculty in the operation of the previous forms of vaporizers arose from the tendency of material having'a higher A `boi1ing point than the desired v apor product to carry over as mist in the form of minute droplets with the separated more volatile vapors. This is objectionable as it results in a condensate having a higher end boilingl point than is desired; I t is an object of our invention to pro'- 4Q vide a vaporizer for use in the refining of petroleum oils, in which the desired vapors are separated from the residuum with an extremely small amount of theA more volatile and valuable hydrocarbons remaining in the residuum.

It is a further object of our invention to provide a vaporizer having a lseries'. ofhorizontally disposed drip screens through which a vertical passageway is provided for collecting the vapors given off between the screens. 1

Another object is to provide'a rye-boiling vat below the evaporating screens for the purpose of re-boiling vthe residuum and driving olf more volatile hydrocarbons therefrom before the residuum is drawn olf from the vaporizer. v

A -further object is to provide a dephlegmating unit inthe top .of the vaporizer for removing mist-like particles of unvaporized material and knocking down less volatile vapors than those desired to be included in the vapor mixture leaving the vaporizer. f

A still further object is to provide a novel hot crude oil distributing element for absorbing the venergy o f movementof the crude oil when discharged into the vaporizer and fequally distributing it over the horizontal drip screens.

Another object is to provide a centrifug or centrifugal separator for removing liquids leaving the vapori er entrained in the vapor and vreturning; the to the vaporizer."

Another object of our invention is to pro- Vide a drip screen of simple construction, which is cheaply constructed, easily installed, and which will lie in a true horizontal plane whenv installed.

Another object is to provide heating and draft accelerating jet-s at various points in the vertical vapor passageway for heating the vapor, and creating a suction from the spaces between the, drip screens around the vertical passageway.

Further objects and advantages will be made apparent in the following description ings, in *which .t Fig. 1 isa diagrammatic view of a portion of a typical petroleum refining apparatus, illustrating the use of our improved va- 300 porizer.

Fig. 2 is a fragmentary vertical medial sectional view of the vaporizer of our invention. y

Fig. 3 is a sectional view taken on the line N5 and claims-and in the accompanying draw- A3- 3of Fig. 2.

Fig. et is a sectional view taken on the line 4-4 of Fig. 2.

Fig. 5 is a sectional view taken on the line 5--5 of 2. y

Fig. 6 is a sectional View taken on the line 6-6 of Fig. 2.

Fig. 7 isa plan view of a dephlegmator unit screen with the screen partially broken away to show 4the frame thereof.

Fig.8 is'a vertical sectional view showing the construction of the novel centrifuge which is a. part of our vaporizer.

Referring to the drawings in detail, Fig.

1o l shows a crude oil pressure pump 10 drawing crude oil through a pipell 'from a crude oil tank (not shown) and -forcing it through a pipe 12, through ahcat exchanger 13, a

pipe 414, anda water separatorl15, .freniV f which a pipe 16 leads the'crude oil to a pipe still20.' Leading from the still 20', a pipe 21 conducts 4the heatedcrude oil and vapors formed therein by heating to the vaporizer 25 embodying our present invention.

I2o The vaporizer 25 has ainain cylindrical i shell 2 6, from the bottom vend of which a\ cylindrical apron l27 extends downwardly 'to provide a support-for the vaporizer, Secured in the apron27 is a bottom plate 28 25 having :..fcentral pening 29, from which a residu'um outlet pipe 30 leads to the heat exchanger 13. Cool residuum is led from the heatexchanger 13 to a storagetank (not shown) by a'pipe 3 5.

A cover 36 closes the upper end of the i shell 26 and is secured thereto by flanges 37 `and 38. lA .vapor-outlet pipe JLG-leads upwardly from an opening41in the center of the coverf36, and enters tangentially the 35 upper portion of the separating chamber 45 f a centrifuge 47 through an` .inverted conlcal shell 48- thereof. An outlet pipe 50 isdisposed vertically in the centerl of the chamber 45 and leads from a short distance above the bottom 51 ofthe shell48 out through the top 52 thereof. A liquid return pipe 53 leads from the bottom 51 throughv a gas trap 55 to the shell 26.

The hot crude oil line 21 connects with a 'l valve 60 which connects to a nipple 61 which passes through and is secured 1n an opening 62 in the shell 26 a short .distance from lthe upper end thereof. Inside the shell 26 anu elbow y65 is secured tothe nipple 61 and connects through anipple 66 to an elbow 67 which has a nozzle nipple 68 pro` jecting therefrom in a direction tangential to the shell 26, as shown in Flg.. 3.

. Supported in a perfectly level. position onv 55 cross bars 70, which attach at their ends to v brackets 71 fixed upon the inside face of opening 62. The elbow turns-down.y

wardly inside the wall 78 sothat the nozzle.

The shell 26 is ldividedvat. 85, a short disi tance below the pan 72 opposing edges of the shell 26 having fianges 86 which are clamped by bolts 87 upon a distributing deck' plate 88. The joint is ,made so that the deck plate 88 will set perfectly level. lVelded into suitable holes in 'the plate 88 are short pipes 90 arranged in concentric .circular rows 91, 92, l93, 94 and 95. The pipes 90 in therows 92, 93 and 95 rise to a uniform height above the plate 88. The pipes 901m the rows 91 and 94 are substantially twice the heightof the pipes 90 in the rows of pipes 92, 93 and '95, and the former have openings formed' in their walls on the same level as the-,upper ends of the rows of pipes 9,2, 93 and 95. l

An overflow pan 101, having a ilat bottom plate 1.02 and low side walls v103'rising therefro1n.at'the outerfedge', rests upon and' is secured tothe upper ends of the rows of pipes 91 and 94.- VVhen the overflw pan 101 is thus secured, there is only" a small space betweenr the upper edge of the wall 103 and'4 the floor 75 of the annular pan 72'.

'Supported horizontally on brackets formed on-the inner surface of the shell 26, beneath thecrude. oil distributing. plate 88, is a' series of uniformly spaced drip screens 105. As shown in Figs. 2 and 5, each of these screens 105 has apair of opposed semii circular angle iron frame halves 106, each ofv which halves comprises a `semi-circular peripheral portion 107 and a diainetral portion 108, the latter being bent 'at the middle .to form va small semifcircular portion 109.

A substantially semi-circular screen 112 is cut to fit within eachlof the frame halves 106, and bolts passing through the vertical fla'nges of the vdiametral portions 108 of opposing frame halves 106 secure the two halves together to forma drip screen 105.

Gripped at its lower end within the circularframe. formed by the semicircular portions l109, when the frame halves 106 are xjoined by the bolts 110 to form the top drip screen 113 ofthe drip screens 105 is ashort cylindrical tube l115. In all the lower screens 105, longer tapered tubes 116 are similarly gripped and held in place. The tubes 1 16 are of such .length that *the upper end ofeach extends a short distance up into the lower end of thetube in the screen immediately above, as shown in Fig.Y 2.

Passing through the shell 26 into the loo space immediately beneath each screen.105

is a valved oilsampl'er 120, a valved vapor sampler` 121, and a` thermometer well 122. Each oil sampler 120 comprises a pipe 125 i, which passes through a nipple 126 formed in oil sampler 120, excepting that the collecting spoon 127 thereof is for collecting vapor instead of oil and consequenty is turned downwardly instead of upwardly.'

The thermometer well 122 comprises a tube 130 which is open at the outer end, at which it passes through and is welded to the shell 26, and which extends obliquely downwardly into the vaporizer 25 and is closed at its lower end.` 'This tube is kept filled` With light lubricating oil.

Stearnjets 135 are disposed in some of the tapered tubes 116 so as to point upwardly. Each of these is supported and supplied with steam by a pipe 136 which threads'into a coupling 137 provided in the shell 26, and which communicates through a nipple 140, a valve 141 and a nipple 142 with a steam manifold line 143. Steam is supplied to the manifold line 14.8 from a boiler 14,4.

A series of twelve to thirty or more of the screens 105 is provided in the vaporizer 25, as shown fragmentarily in Fig. 2. Beneath the lowermost screen 105 is a re-boiliug vat fill 150 having the plate 28 as a bottom and apron 27 as sides.

A standard liquid level gage 151 communicates with a vertical pi e 152 which communicatesat the top-and ottom ends thereof through pipes 153 and 154 With the .reboiling vat 150, so that,the level of liquid in the vat will be indicated by the gage 151.

Lying in a central positionupon the floor 28 of the re-boiler 150 is a live steam heating element 160. This element is formed of a circular pipe 161 perforated at 162,0n its upper face. Opposite endspf the pipe 161 are welded into opposite ends of a T-fitting 165 which commnunicates through a pipe 166, a threaded coupling 1,67 provided in the the ' apron 27 a nipple 168, a valve 169 and a nipple 170, with the steam line 143.

In the shell 26,-just above the opening 62, is a horizontal screen 175. rlhis screen is mounted in the same manner as the screens 105, and as shown in Fig. 7 is identical in structure therewith excepting that the diametral cross bars 176 are straight throughout their length and the screens 177 are cut to lit the frame halves 178 and lie flat therein. The cross bars 17 6 are securely bound together by bolts 179.

Mounted in the shell 26 about one-half its diameter above the screen 175 andan equall distance below the top of the shell 26 is any identically similar screen 185. This screend 185 supportsfa mass of dephlegmating steel turnings or kinked wire 186, which fills the space above the screen 185 upto the opening 41 in the vaporizerycap 36'. l

The operation ofour improved vaporizer when operating upona certain grade of California oil is as follows.:

The hot oil from the pipe still 2O enters the vaporizer 25 at about 500 F. through the pipe 21, the valve60, the nipple 61, the

elbow 67 and is projected from the nozzle 68 tangentially into the annular pan 72.

Under certain conditions of operation, this oil will contain bubbles of vaporsproduced by distillation from the oil in the pipestill 20. The mixture thus discharged rapidly fills the `annular basin in this pan. and

overflows the wall 79, passing downwardly through the 'opening 200 surrounded thereby into the voverflow pan 101. The tangential discharge of oil and vapor` through the nozzle 68 also causes a rapidly rotating current in the annular basin 80. The Wall 78, \however, is of such height thatv the liquid will not build up sufficiently againstit, due to the centrifugal force, to overflow this wall, but instead will overflow entirely through the opening 200. In this rapidly rotating mass of liquid the kinetic energy of the incoming oil is absorbed, and oppor-l tunity is now given for a uniform distribution of the liquid with its .entrained vapor bubbles over the entire cross sectional s ace of the vaporizer. This is accomplishe by the flowin of the mixture over the outer wall 201 o the pan 101 upon the distributin1 deck 88.

he level of liquid on the deck 88 rises until it is above the tops of the pipes 90 i-n lthe rows 92, 93 and 95, which level is also above the bottoms of openings ,100 in the `other pipes 90. Thus'the 4rising mixture flows equally down through all of the pipes 90 and causes a uniform distribution of the mixed oil and vapor over the top drip screen 113. The mixture then drips uniformly from ,this screen to the screen below it, and so im through the whole series of screens 105.

underneath the deck plate 88. From-here.

the vapors passupwardly through the tubes 90 and through the space 207,

rbetween the walls 78 and tlieshell 26. Above the pan T 2 the vaporspass-througli the screen 175, i

the screen 185, the mass of dephleginating material 18,6. and out from 'the vaporien `through thevapor line 40.A f I WVhen it is desired to .accelerate this vapor i steam is' admitted through the' Passage, 'vali/c5141 to they nozzles 135.' The resulting jets of steam directed upwardly in the piassageway 205 draw an increased amount of p vapor'from the surrounding space and cause screens 175 and tur'nngs 186, condenses and collects any vapors heavier than those desired to-pass 'out with the vapor mixture. These condensates dropdown and pass ythroughthe vaporizer with the 4fresh intlux'of oil, eventually finding their way into the re-boiler 150 with the residuum. y

4 The Aresiduum is drawn olf through the pipe at such a rate as to maintain the level in the re-boiler 150 whereitwill be visible in the gage 151. Frequent testsare made of the initial boiling point of the residuum thus drawn od, and if anyptest shows that prod# ucts desired .to be'vaporized are passing .out

of thevaporizer with theresiduum, the valve-v 169 is. opened and live steam admitted into the'- residuum lin there-boiler 150 through the perforated pipe 160. This re-boilsl theresiduum and lowers thepartial vapor pres- ,sure"therein,'causing the more volatile hy-r drocarbons to Vbey vaporized from the :re-

' 4-siduum.

` vaporl and the temperature The natureof the oil, the' nature of the of the vaporizer or all'the drip lmay be noted beneath any i' i screens 105 at regular .intervals during the operation ofthe vaporizer, or only when specialA grades of crude oil are being run.

To obtain a'ii oil sample from any oil sam'- pler 120- the valve 128 thereof is openednnd Vthe oil collecting in the spoon 127 'will run outthrough the pipe'125 into a receptacle '(not shown) held to receive it. '-A vapor sample fromany vapor-sampler 121 may be i V,obtained in a sinilar manner. .Aiiopenmouthedvessel is inverted and `placed above the outer vendof'th'e pipe 125 ofa lvapor sampler121 and with'the mouth of the vessel communicating therewith.v -The valve 128 thereof will then be opened.` Vapor rising inside the vaporizer. 25 will be collected bythe vapor spoon 129, passthrough the vapor sampler 1,21 and rise-into the. receiving verf sel. lVhen the vessel is full of fvapor, it

shut olf. .p l

To test the-temperature, a thermometer Ais placed in -the'oil in a'well 122 and removed after a sufficient period of time for reading.

should be quickly closedand thel valve 128 The centrifuge' 47 is not essentially a part of the vaporizer 25 but has proved to be a valuable accessory used in conjunction therewith, ywhen certain classes ofcrude oil are being run.

The centrifuge 47- is combined with they vaporizer 25 for the removal of any particlesof liquid which may be mechanically entrained in the vapors leaving the vaporiz-er and returning these liquidsfor further treat ment inthe vaporizen This separation of liquids from the vapor mixture isaccomfuge a hydrocarbon va'porizer or vapor separator nvliich permits of perfect control of vaporization in such manneras to keep the initial boiling point of the residuum above a preiplished by thecentrifugal force sct'iip by rapidrotation of the vapors in the centrilt'will thus be seen that we have produced determined minimum and the end point Qt', f5

the liquids vaporized bei-ow a .predetermined maximum. Also the means for acceleratingthe flow of vapfirs through the collecting passageway 205 increases the activity of the vae I i porizer and greatly increases the efficiency andl capacity of a unit of given size- The testing means at different stages of the de! scent of oil through theA vaporizer also permits keeping perfect-control of the process and maintaining its operation at `the highest possible efficiency. I

f We claim as our invention: .i i.

` 1. A vapor separator comprising: a shell;` means for admitting hot oil into the top por- 'ins tionof said shell; a series of foraminousl members securedA in said shell; means for distributing said incoming hot oil uniformly over said foiaminous members; a series of sleeve members, each centrally secured to oneA of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminoiis member; and means for withdrawing vapor from the topinost of said sleeves.

miY

2. A vapor separatoroomprisiiigza shell;

means for`admitting hot oil into the top portion of said-shell; a seriesof foraminous members secured in said shell; means for distributing said incominghot oil uniformly over said'for'amin'ous members; a series of sleeve members, each centrally securedto one of said foraminous members and extending .12,5

upwardly therefrom into a sleeve of the next higher foraminous member; means for artificially producing an upward draft throughA said' sleeves; andy means for withdrawing vapor from the topmost of said sleeves.

3, A vaporl separator comprisngzashell;

means for admitting hot oil into the top portion of said shell; a series of foraminous members secured in said shell; means for distributing said incoming hot oil uniformly tion of said shell; a series of foraminousV over said foraminous members; a series of sleeve members; each centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; steam jets so situated as to produce an upward draft through said sleeves; and means for withdrawing vapor from the topmost of said sleeves.

Il. A vapor separat-or comprising: a shell; means for admitting hot oil into the top portion of said shell; a series of foraminousl members secured in said shell; means for distributing said incoming hot oil uniformly over. said foraminous members; means for maintaining a body of residuum in the bottom of said shell belovv7 the lowest of said members; means for heating said body of residuum; a series of sleeve members, each centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher `foraminous member; and means for withdrawing vaporl from the topmost of said sleeves.

5. A vapor separator comprising: a shell; means for admitting hot oil into the top pormembers secured in said shell; means for distributing said incoming hot oil uniformlyv over said foraminous members; means for maintaining a body of residuum in the bottom of said shell below thelowest of said members; means for heating said body of residuum; a series of sleeve members;each

centrally secured to one of said foraminous members and extending upwardly therefrom g into a sleeve of the next higher foraminous member; means for artificially producingl an upward draft through said sleeves; and

means for withdrawing vapor Vfrom the topmost of said sleeves. f

6. A vapor separator comprising: a shell; i'

. centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher 'forammous member; steam jets so situated as to produce an upward draft'through said sleeves; and

means for withdrawing vapor from the topmost of said sleeves. l

7 AJ vapor separator comprising: a shell;

means for 'admitting hot oil into the top .portion of said shell; a series of foraminous f higher foraminous member;and 'means for 'opmost of .said

withdrawing vapor from that sleeves. v e

8. A vapor separator comprising: a shell; means for admitting hotv oil' into the top portiony of said'shell; a vseriesvof foraminous members secured'in saidshell; means for distributing said incoming -hot oil uniformly over said foraminous members; means for maintaining a body of residuum in thebottom of said shellbelow' the lowest of said members; a steam pipeso placed as to inject cksteam into'said body/of residuum for heating said body `of residuum; a series of sleeve members, each centrally secured to one of said foraminousmembers and extending upwardly therefrom intoa sleeve of the next higher foraminous member; means* for artificially producing an upwarddra'ft through said sleeves; and means forY withdrawing vapor from the. topmost of said sleeves.

9. A vapor lseparatorcomprising:a shell; means for'adm'itting hot oil into the top portion of said shell; a series of foraminous members secured in said shell; means for V.distributin said'incoming hot oil uniformly Lover said oraminous members;; means for lmantaining'a body of residuum] in the botof said shell below the lowest of said ynembers; a steam pipe so placed as to inyj 'eetsteam into said body of residuum for heating said body of residuum; a series of sleeve',-'members, each centrally secured to one ofsaid foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; steam jets so situated as to produce an upward draft through said sleeves; and means for with *drawing` vapor from the topmost of said sleeves.

10. A vapor separatorcomprising: a shell; means for admitting hot oil into the top portion of said shell; a series of foraminous members secured in said shell; means for distributing said incoming hot oil uniformly over said foramino'us members; a series of sleeve members, each centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; a mass of metallic material having small continuous passages therethrough situated above said from above said mass.

11. A vapor` separator comprising: ya shell; means for admitting hot oil into the top portion of said shell; a series of forami-` nous members secured in said shell; means for distributing said incoming hot oil uniformly over said foraminous members; 4a series of sleeve members, each centrally seand extending upwardly therefrom into -a sleeve of the next higher foraminous member; means for artificially producing an upwardl draft through said sleeves; al mass 0f metallic,material havin(T4 small continuous passages therethrough situated above said means for admitting hot oil into the top of said shell; and means for withdrawing vapor from above said mass.A l

12. A vapor separator comprising: a

j shell; means for admitting hot' oil into vthe top portion of said shell; a series of foraminous members secured in said shell; means. for

distributing said incoming hot oil uniformly over said foraminous members; a series of sleeve members, each centrally ,secured to one of said foraminous members and extending upwardly Vtherefrom into a sleeve of the next higher foraminous member steam `jets so situated as to produce an' upward draft through said sleeves; a massof metallic material having smallI continuous passages or therethrough situated above said means admitting hot oil into thetop of said shell;

and means for withdrawing vapor from above said mass'.

13. A vapor separator comprising: a shell; means for admittingl hot oil into the top portion of said shell; a series of'foraminous members secured in said shell; means for distributing .said incoming hot oil uniformly over said foraminous members; means for maintaining a body of residuum in the bottom of saidK shell below the lowest of said members; means for heating said body of residuum; a series of sleeve members,oeach centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; a mass ,of metallic material having small continuous passages therethrough situated abovepsaid means for admitting hot oil into the top of said shell; and means for withdrawing vapor from above said mass.

14. A l vapor separator epmprising: a

shell; means for admitting hot oil into the means for maintaining a body of residuum in the bottom of said shell below the lowest -of vsaid members; means for heating said body of residuum; a series of sleeve mem 'tom of sai .'members; a steam pipe'so placed' as to inject bers, each centrally secured to one ofvsaid foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; means for artificially producing an upward draft through said Sleeves; a mass of metallic material having small continuous passages therethrough situatedV above said means for admitting hot oil into the top of said shell; and means for ,withdrawing vapor from above said mass. cured to one of said foraminous members,

inous members and extending upwardly therefrom into a lsleeve ofthe next higher foraminous member; steam jets so situated as to produce an upward draft through said lll) sleeves; avmass of metallicmaterial having small v.continuous passages therethrough situ ated above saidrmeans for admitting hotoil into the top of said shell; and means'for withdrawing vapor from above said mass.

16. A vapor separator comprising: a shell; means for admitting hot oil-into the top portion of said shell; a series of foraminous members securedv in said shell; means for distributing said incoming hot oil uniformly over said foraminous members; means for maintaining a body of resfiduum in the bottom of said shell below 4the lowest of said members; a steam pipe soplaced as to inject stea'm into said body of residuumI for heating said body ofresiduum; a series of sleeve members, each centrally secured to one 'of said foraminous-members and extending upwardly therefrom into a sleeye of the next higher foraminous member; a mass of metallic material having small continuous passages therethrough situated above said means for admitting hot oil into the top of said shell; -and mea-nsl for withdrawing4 vapor from above'said mass. a

17. A vapor separator comprising: a shell; means for admitting hot oil int-o the top portion of said shells a series of foraminous members secured in 'said shell; means for distributing said incoming hot oil uniformly over said foraminous members; .means for maintainin a body of residuum in thebotshell below the -lowest of said steam into saidbody of residuum for heating said body of residuum; a series of sleeve members, eachI centrallygsecured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; means for artimembers secured in said shall; means'for distributing said incoming hot oil uniformly over said foraminous members; means for maintaining a body7 of residuum in the bottom of said shell below the lowest of said members; a steam pipeyso placed as to inject steam into said body of residuum for heating said body of residuum'; va series of sleeve members, each centrally secured to one of said foraminous members and extending upwardly therefrom into a sleeve of the next higher foraminous member; steamv jets so situated as to produce an upward draft through said sleeves; a. mass of metallic material having small continuous passages therethrough situated above said, means for admitting hot oil into the tp of said shell; and means for vwithdrawing vapor from above said mass.

19. A vapor 'separator comprising: a shell means for admitting hot oil into the top portion of said shell; a series of foraminous members secured in said shell; means for distributing said incoming hot oil uniformly over saidforaminous' members; a series of sleeve members, each centrally secured to one of said foraminous members and extendi' ing upwardly therefrom towards a sleeve of the next higher foraminous member so that said sleeves form` a substantially continuous passageway centrally through said foraminous members, which passageway communi- Cates with the spaces between adjacent pairs of foraminous members; and means for withdrawing vapor from the topmost of said sleeves.

20. A vapor separator'comprising: a shell; means for admitting hot oil into the top portion of said shell; a series of foraminous members secured in said shell; means for distributing said incoming hot oil' uniformly over said foraminous members; .a series of sleeve members, each centrally secured to one of said foraminous members and extending upwardly therefrom towards a sleeve ofthe next higher foraminous member, so that said sleeves form a substantially continuous passageway centrally through said foraminous members, which passageway communicates with the spaces between adjacentpairs of foraminous members; means for artificially prod ucing an upward draft through said sleeves; and means for withdrawing vapor from the. topmost of said sleeves.

21. A vapor separator comprising: a.' shell; means for admitting hot oil into the top portion of said shell a series of foraminous members secured in said shell; means for distributing said incoming hot oil uniformly over said foraminous members; a series of sleeve members, each centrally secured to one of said foraminous members and extending upwardly therefrom towards a sleeve of the next higher foraminous member so that said sleeves form a substantially continuous passageway centrally through said foraminous` sleeves; and means for withdrawing vapor` from the topmost of said sleeves.

.In testimony whereof, we have hereunto set our hands at Los Angeles, California,

vthis 24 dayof December, 1925.

FRANK A. MILLIFF. JOHN A. MILLIFF. 

